• Title/Summary/Keyword: 산화환원반응

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생물전기화학적 기술을 이용한 물질 전환

  • 김병홍
    • The Microorganisms and Industry
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    • v.17 no.2
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    • pp.18-21
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    • 1991
  • 생물은 자기 복제를 통한 생장이나 생명유지를 위해 에너지를 필요로 한다. 화학영양생물은 화학에너지를 발효 혹은 호흡을 통해 생물학적 에너지로 전환시키며, 광영양생물은 광합성 작용을 통해 광에너지를 이용한다. 발효, 호흡, 광합성은 모두 산화-환원 반응을 통해 이루어진다. 생물의 모든 에너지 전환반응은 산화-환원 반응, 즉 전자의 흐름으로 이루어지며 생명현상이 에너지를 필요로 하기 때문에 생명현상은 전자의 흐름으로 이루어진다고 할 수 있다. 모든 생물이 에너지 전환 반응에 산화-환원 반응을 이용한다는 말은 생물이 많은 종류의 산화-환원 효소를 보유하고 있다는 뜻이며, 실제 많은 종류의 산화-환원 효소가 발견되고 연구되었다.

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LiCl 용융염 전해환원 공정 희토류원소 산화물의 화학적 거동

  • Park, Byeong-Heung;Choe, In-Gyu;Jeong, Myeong-Su;Heo, Jin-Mok
    • Proceedings of the Korean Radioactive Waste Society Conference
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    • 2009.11a
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    • pp.346-346
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    • 2009
  • 산화물 형태 사용후핵연료의 효율적 처분 혹은 재활용을 위한 연구 가운데, 고온의 LiCl 용융염 중에서 전해환원하여 금속으로 환원시킨 후, 환원된 금속을 고온의 LiCl-KCl 용융염에서 전해정련하는 연구가 국내외적으로 활발하게 진행되고 있다. 전해환원을 위해 일정 농도 $Li_2O$가 LiCl 용융염에 첨가되며 $Li_2O$ 농도가 높으면 반응 재질의 부식성이 크게 증가하므로 일반적으로 우라늄 산화물은 1wt% 이하의 $Li_2O$ 농도에서 전해환원 된다. 우라늄 산화물의 전해환원 전위는 $Li_2O$의 전해환원 전위 보다 표준 상태를 기준으로 공정온도인 650 $^{\circ}C$ 에서 약 70 mV 정도 낮기 때문에 전해환원 과정에서 $Li_2O$ 의 환원으로 Li 금속이 생성될 가능성이 있으며 우라늄 산화물은 대부분 직접 전해환원 되지만 일부 Li에 의해 화학적으로 환원되기도 한다. 전해환원 공정에서 환원되지 않은 희토류 산화물은 전해정련 공정에서 $UCl_3$와 반응하여 $UO_2$를 생성시켜 공정 효율을 떨어뜨린다. 따라서 전해환원 공정에서 가능하연 최대한 희토류 산화물을 금속으로 환원시키는 조건을 찾아내는 것이 바람직하고 이를 위해서 우선 전해환원 공정에서 희토류 산화물의 화학적 거동의 이해가 요구된다. 본 연구에서 열역학적 검토를 통하여 희토류 산화물의 환원 조건을 조사한 결과 희토류 산화물은 매운 낮은 $Li_2O$ 농도에서 Li에 의해 환원되고, 1wt% 이하의 $Li_2O$ 농도에서는 Sc와 Lu의 산화물이 $Li_2O$와 복합산화물을 형성하고 이들 복합산화물은 Li에 의해 환원되지 않는 것으로 나타났다. 또한 희토류 원소 별로 희토류 원소 산화물의 Li에 의한 환원 조건으로서 평형상태에서의 $Li_2O$ 농도 즉 환원 임계 $Li_2O$ 농도를 실험적으로 측정하였으며 1wt% $Li_2O$ 농도 이하에서 열역학적 해석과 동일하게 Sc와 Lu만이 복합산화물을 형성하여 Li에 의해 직접환원 되지 않는 것으로 관찰되었다.

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Analysis of Oxidation-reduction Equilibria in Aqueous Solution Through Frost Diagram (Frost도를 이용한 수용액의 산화-환원반응 평형 해석)

  • Lee, Man Seung
    • Resources Recycling
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    • v.26 no.4
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    • pp.3-8
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    • 2017
  • Oxidation-reduction reaction is one of the most important reactions occurring in the aqueous phase. Analysis of the equilibria related to these oxidation-reduction reactions is of great value in designing many unit operations in hydrometallurgy, such as leaching, separation and electrochemical reactions. The construction of Frost diagram was discussed in this work. The conditions at which disproportionation and proportionation reactions can occur were explained by analyzing Frost diagram together with Latimer table. The information which can be obtained from Frost diagram was discussed.

Catalytic Reduction of Oxidized Mercury to Elemental Form by Transition Metals for Hg CEMS (수은 연속측정시스템에서 전이금속에 의한 산화수은의 원소수은으로의 촉매환원)

  • Ham, Sung-Won
    • Clean Technology
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    • v.20 no.3
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    • pp.269-276
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    • 2014
  • This study was aimed to develop catalytic system for the dry-based reduction of oxidized mercury ($Hg^{2+}$) to elemental mercury ($Hg^0$) which is one of the most important components comprising mercury continuous emission monitoring system (Hg-CEMS). Based on the standard potential in oxidation-reduction reaction, transition metals including Fe, Cu, Ni and Co were selected as possible candidates for catalyst proceeding spontaneous reduction of $Hg^{2+}$ into $Hg^0$. These transition metal catalysts revealed high activity for reduction of $Hg^{2+}$ into $Hg^0$ in the absence of oxygen in reactant gases. However, their activities were greatly decreased in the presence of oxygen, which was attributed to the transformation of transition metals by oxygen to the corresponding transition metal oxides with less catalytic activity for the reduction of oxidized mercury. Hydrogen supplied to the reactant gases significantly enhanced $Hg^{2+}$ reduction activity even in the presence of oxygen. It might be due to occurrence of combustion reaction between $H_2$ and $O_2$ causing the consumption of $O_2$ at such high reaction temperature at which oxidized mercury reduction reaction took place. Because the system showed high activity for $Hg^{2+}$ reduction to $Hg^0$, which was compatible to that of wet-chemistry technology using $SnCl_2$ solution, the catalytic reduction system of Fe catalyst with the supply of $H_2$ could be employed as a commercial system for the reduction of oxidized mercury to elemental mercury.

Thioredoxin-Mediated Regulation of Protein Synthesis by Redox in Saccharomyces cerevisiae (Saccharomyces cerevisiae에서 산화환원에 의한 In Vitro 단백질합성의 Thioredoxin에 중재된 조절)

  • Choi, Sang-Ki
    • Microbiology and Biotechnology Letters
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    • v.35 no.1
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    • pp.36-40
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    • 2007
  • Redox signaling is one of way to regulate growth and death of cell in response to change of redox of proteins. To search whether translation is regulated by redox, we attempted in vitro translation assay under condition with or without DTT. Interestingly in vitro translation activity was increased up to 40% In the presence of dithiothreitol (DTT). Then we checked whether this positive effect by DTT was further accelerated by addition of thioredoxin (Trx). When a Trx purified from Saccharomyces cerevisiae was added to the in vitro translation extract, we observed a dose-dependent increase in translational activity. These results suggest the possibility of translation factors being redox-regulated via Trx in vivo.

Redox Property of Transition Metal Oxides in Catalytic Oxidation (TPR/TPO 실험기법을 이용한 전이금속산화물의 산화-환원 특성 연구)

  • Kim, Young-Ho;Lee, Ho-In
    • Applied Chemistry for Engineering
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    • v.10 no.8
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    • pp.1161-1168
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    • 1999
  • The redox property of oxide materials of the 3rd period transition metals(Cr~Zn), V, Mo, and W was studied with temperature-programmed reduction/temperature-programmed oxidation(TPR/TPO) experiment. The peak temperatures of TPO spectra were equal to or lower than those of TPR spectra. And the peak shapes of TPO spectra were broader than those of TPR ones. The activation energies of TPR/TPO for the oxides of the 3rd period transition metals showed in the range of 33~149 kJ/mol, while for the oxides of V, Mo, and W, they showed relatively higher values. The change of activation energies of TPR/TPO with various metal oxides showed a similar trend to the change of their metal-oxygen bond strengths. The change of activation energies of o-xylene oxidation for various metal oxides was proportional to the difference (${\Delta}E_a$) between the activation energy of TPR and that of TPO. From these results, we concluded that the oxidation of o-xylene over various metal oxide catalysts follows the Mars-van Krevelen mechanism including the surface reduction-oxidation of the metal oxide itself.

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Morphological Effect of Hematite on the Synthesis of Fayalite in Reducing Atmosphere (환원성 분위기에서의 규산철의 합성에 미치는 산화 제2철의 형태학적 효과에 관한 연구)

  • 임응극;권명수
    • Journal of the Korean Ceramic Society
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    • v.12 no.4
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    • pp.37-42
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    • 1975
  • 철(II)이온을 안정화 하기위하여, 2산화 규소와, 구상, 입방체상 및 침상의 서로 다른형태의 산화 제2철로부터 규산철을 합성하였다. 메타놀증기로 포화시킨 질소까스를 튜브로에 도입시켜 얻은 환원성 분위기속에서, 114$0^{\circ}C$에서 11$65^{\circ}C$의 온도범위에서, 가스유속을 0.13 및 0.25l/min. 로서, 환원시간 4-150분동안 교상반응을 진행하였다. 반응생성의 동태를 오르자트 가스분석으로 검토하였으며, 생성물의 확인은 X-선 회절시험 및 감량정량에 의하였으며, 결과는 다음과 같다. 1 : 1.1의 몰비로 혼합한 산화제2철과 2산화 규소의 경우, 가스유속이 0.13l/min일 때, 규산철 합성반응시간은 구상, 입방체상 및 침상산화철에 있어서 각기 8-27분, 10-16분 및 6-7분으로 구상의 경우가 범위가 가장 넓었다. 또한, 반응속도는 산화제2철의 표면적의 평방근에 비례하였고 반응시간의 평방근에 역비례하였다.

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Microbial Reduction of Iron Oxides and Removal of TCE using the Iron Reduced by Iron Reducing Bacteria (철 환원 박테리아에 의한 산화철의 환원과 환원된 철을 이용한 TCE 제거에 관한 연구)

  • Shin, Hwa-Young;Park, Jae-Woo
    • Journal of Korean Society of Environmental Engineers
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    • v.27 no.2
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    • pp.123-129
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    • 2005
  • In situ permeable reactive barrier (PRB) technologies have been proposed to reductively remove organic contaminants from the subsurface environment. The major reactive material, zero valent iron ($Fe^0$), is oxidized to ferrous iron or ferric iron in the barriers, resulting in the decreased reactivity. Iron-reducing bacteria can reduce ferric iron to ferrous iron and iron reduced by these bacteria can be applied to dechlorinate chlorinated organic contaminants. Iron reduction by iron reducing bacteria, Shewanella algae BrY, was observed both in aqueous and solid phase and the enhancement of TCE removal by reduced iron was examined in this study. S. algae BrY preferentially reduced Fe(III) in ferric citrate medium and secondly used Fe(III) on the surface of iron oxides as an electron acceptor. Reduced iron formed reactive materials such as green rust ferrihydrite, and biochemical precipitation. These reactive materials formed by the bacteria can enhance TCE removal rate and removal capacity of the reactive barrier in the field.

The Influence of Mental Capacity and Understanding of the Oxidation Reduction Concepts on Senior and Science High School Students' Completion of the Balancing Redox Equations (일반고와 과학고 학생들의 정신용량과 산화 환원 개념의 이해도가 산화 환원 반응식 완결에 미치는 영향)

  • Choe, Byeong-Sun;Kim, Chung-Ho;Lee, Sang-Gwon
    • Journal of the Korean Chemical Society
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    • v.46 no.4
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    • pp.345-353
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    • 2002
  • The purpose of this study was to analyze the influence of mental capacity and understanding of the oxi-dation-reduction concepts on the completion of the balancing redox equations. Participants were 92 senior high school students and 57 science high school students. Tests were conducted to measure the mental capacity, the understanding of the oxidation-reduction concepts and the completion of the balancing redox equations and the influence on the per-formance was analyzed. The performance of the senior high school students increased as the mental capacity increased, but the performance of science high school students did not change by mental capacity. Most of senior high school stu-dents couldn't understand the oxidation-reduction concepts well. Most of science high school students, however, under-stood the concepts completely and partially. The students who had a good understanding of the oxidation-reduction concepts showed a good performance for both senior and science high school students, regardless of the problem pattern.

Carbothermic Reduction of Zinc Oxide with Iron Oxide (산화아연(酸化亞鉛)의 탄소열환원반응(炭素熱還元反應)에서 산화철(酸化鐵)의 영향(影響))

  • Kim, Byung-Su;Park, Jin-Tae;Kim, Dong-Sik;Yoo, Jae-Min;Lee, Jae-Chun
    • Resources Recycling
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    • v.15 no.4 s.72
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    • pp.44-51
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    • 2006
  • Most electric arc furnace dust (EAFD) treatment processes to recover zinc from EAFD employ carbon as a reducing agent for the zinc oxide in the EAFD. In the present work, the reduction reaction of zinc oxide with carbon in the present of iron oxide was kinetically studied. The experiments were carried out at temperatures between 1173 K and 1373 K under nitrogen atmosphere using a weight-loss technique. From the experimental results, it was concluded that adding the proper amount of iron oxide to the reactant accelerates the reaction rate of zinc oxide with carbon. This is because iron oxide in the reduction reaction of zinc oxide with carbon promotes the carbon gasification reaction. The spherical shrinking core model for a surface chemical reaction control was found to be useful in describing kinetics of the reaction over the entire temperature range. The reaction has an activation energy of 53 kcal/mol (224 kJ/mol) for ZnO-C reaction system, an activation energy of 42 kcal/mol (175 kJ/mol) for $ZnO-Fe_{2}O_{3}-C$ reaction system, and an activation energy of 44 kcal/mol (184 kJ/mol) for ZnO-mill scale-C reaction system.